Rare earth element-doped perovskite-type Ru-loading ammonia-synthesis catalyst
A rare earth element and perovskite type technology, which is applied in the direction of catalyst carrier, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of no industrial promotion and application value, low ammonia synthesis activity, Reduce the problems of catalyst stability and life, and achieve the effects of inhibiting hydrogen adsorption, reducing the amount of precious metals, and improving the activity of low-temperature and low-pressure ammonia synthesis
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Embodiment 1
[0041] Ba(NO 3 ) 2 : Zr(NO 3 ) 4 . 5H 2 O: Y(NO 3 ) 3 . 6H 2 O: The mixture with the molar ratio of citric acid 1:0.9:0.1:3.0 was dissolved in an appropriate amount of distilled water to obtain a colorless clear viscous liquid. The solution was slowly heated in a water bath at 80°C for 4 h to evaporate excess water, and then heated at a constant temperature of 90°C for 12 h to promote the gelation of the mixture. Finally, the obtained yellow gel was calcined at 300 °C for 1 h to obtain the precursor, and then calcined at 1000 °C for 10 h to obtain the BaZr 0.9 Y 0.1 o 2.95 carrier material. The active component ruthenium was impregnated into the carrier by equal volume impregnation method, and then reduced with absolute ethanol. The active component Ru accounted for 2% of the mass fraction of the carrier. The catalyst is at 3 MPa with a space velocity of 10000 h -1 At 350°C, 375°C, 400°C and 425°C, the outlet ammonia concentrations were 2.42%, 5.80%, 7.86% and 7....
Embodiment 2
[0043] Catalyst preparation method is the same as embodiment 1, but BaZr 0.9 Y 0.1 o 2.95 The calcination temperature of the precursor is 800°C, and other conditions are the same. Get BaZr 0.9 Y 0.1 o 2.95 The specific surface area is 9.97m 2 .g -1 , the ruthenium catalyst was obtained by equal volume impregnation method. At 3 MPa, the air velocity is 10000 h -1 At 350°C, 375°C, 400°C and 425°C, the outlet ammonia concentrations were 2.13%, 4.72%, 7.03% and 7.69%, respectively.
Embodiment 3
[0045] Catalyst preparation method is the same as embodiment 1, but BaZr 0.9 Y 0.1 o 2.95 The calcination temperature of the precursor is 1100°C, and other conditions are the same. Get BaZr 0.9 Y 0.1 o 2.95 The specific surface area is 6.69m 2 .g -1 , the ruthenium catalyst was obtained by equal volume impregnation method. At 3 MPa, the air velocity is 10000 h -1 At 350°C, 375°C, 400°C and 425°C, the outlet ammonia concentrations were 0.46%, 0.92%, 2.06% and 4.15%, respectively.
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